US4178950A - Residual fuel compositions with low pour points - Google Patents

Residual fuel compositions with low pour points Download PDF

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US4178950A
US4178950A US05/949,915 US94991578A US4178950A US 4178950 A US4178950 A US 4178950A US 94991578 A US94991578 A US 94991578A US 4178950 A US4178950 A US 4178950A
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residual fuel
ethylene
propylene
vinyl acetate
terpolymer
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William M. Sweeney
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Texaco Inc
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Texaco Inc
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/192—Macromolecular compounds
    • C10L1/195—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/197—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid
    • C10L1/1973—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid mono-carboxylic
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17D—PIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00—Pipe-line systems
    • F17D1/08—Pipe-line systems for liquids or viscous products
    • F17D1/16—Facilitating the conveyance of liquids or effecting the conveyance of viscous products by modification of their viscosity
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00—Fluid handling
    • Y10T137/0318—Processes
    • Y10T137/0391—Affecting flow by the addition of material or energy

Definitions

  • This invention is concerned with means for providing a low sulfur, low pour fuel oil composition. More particularly, the invention is concerned with a fuel oil composition containing a major amount of a high pour, low sulfur, waxy residual fuel and a minor amount of a low wax, low pour, residual fuel oil, this blend having a reduced pour point relative to its components owing to the incorporation therein of a minor amount of an oil-soluble terpolymer or graft copolymer.
  • residual fuel oils contain quantities of wax and asphaltic compounds which render them viscous and which sometimes interfere with practical use thereof. Particularly serious problems can be encountered in pumping residual fuel oils to a burner and in making them flow at low temperatures. Other factors to be reckoned with in regard to these oils are the facts that they behave as non-Newtonian liquids at low temperatures; exhibit variable solidifying temperatures and manifest peculiar hysteresis phenomena--all of which result in difficulties in equipment design.
  • additives in lubricating oils and in so-called middle distillates in order to tie in the wax present therein and to improve flow characteristics at reduced temperatures.
  • the additives in question consist either of compounds formed by alkylating benzene or naphthalene derivatives; or, of copolymers of ethylene-vinyl fatty acid ester of a molecular weight up to 3,000 containing from 15 to 25 percent by weight of the vinyl fatty acid ester.
  • the main object of the present invention accordingly, is to provide for critical blending of high pour waxy residual fuel oils with low waxy, low pour residual fuel oils to give large increases in pour reduction without employing elaborate dewaxing procedures.
  • An equally important object of the claimed invention is to provide a novel fuel oil blend characterized by a low sulfur content and a reduced pour point resulting from the incorporation therein of a small amount, for example, a terpolymer of vinyl acetate, ethylene and propylene or butylene.
  • a further object of the claimed invention is to provide a fuel oil blend which will be stable at different blend temperatures over prolonged storage times.
  • this invention relates to fuel oil compositions having low pour points comprising a major amount of a high pour, low sulfur, waxy residual fuel, and a minor amount of a low wax, low pour residual fuel containing an effective pour depressant amount of an oil-soluble terpolymer or a graft copolymer.
  • the terpolymer used in preparing the crude oil compositions of this invention is a vinyl acetate-ethylene, propylene or butylene terpolymer while the graft copolymer comprises an ethylene-vinyl acetate backbone or basic chain having grafted thereto propylene or butylene.
  • this invention relates to a process for the pipeline transportation of the above-described fuel oil compositions.
  • the residual fuel oil composition of this invention comprises a major amount (i.e., over 50 percent by volume) of a high pour, low sulfur waxy, residual fuel oil having an API gravity of about 20.0 to about 25.0; a sulfur content of between about 0.40 wt. % and about 0.96 wt. %; a Furol viscosity at 122° F. of about 60 to about 230; a flash point of between about 300° and 450° F., with a wax content of between about 10 and 20 percent; and a minor amount (i.e. less than 50 percent by volume) of a low waxy, low pour residual fuel oil having an API gravity of about 10.0 to about 15.0; a Furol viscosity at 122° F.
  • a waxy, low pour residual fuel oil which has given particularly good results as the minor constituent of the claimed blend is that known as No. 6 Fuel Oil (Is this Louisiana No. 6?) which has an API gravity of about 12.3, a Furol viscosity of 207.0 at 122° F., a pour point of about 40° F. and a wax content of about 3 percent.
  • the residual fuel oil compositions of this invention will contain about 55 to about 85 volume percent of the high pour, low sulfur, waxy residual fuel; about 45 to 15 volume percent of the low wax, low pour residual fuel and about 0.01 to about 0.5 weight percent of the oil soluble terpolymer or graft type copolymer.
  • One type of oil-soluble terpolymers useful in preparing the crude oil compositions of this invention comprises recurring units of vinyl acetate, ethylene and propylene or butylene.
  • the number average molecular weight of the vinyl acetate-ethylene-propylene or butylene terpolymer utilized in this invention as previously described will range from about 5000 to about 80,000 or more and preferably will be from about 12,000 to about 60,000 as determined by vapor pressure osmometry.
  • the weight percent of the vinyl acetate units is about 10 to about 45; the weight percent propylene or butylene units is about 0.01 to about 5.0 with the ethylene units being the balance.
  • Preparation of the vinyl acetate-ethylene-propylene or butylene terpolymer is conducted using processes well known in the art. For example, ethylene, vinyl acetate, and propylene in benzene are reacted in a stirred autoclave at a temperature of about 130° to about 150° C. and under pressures ranging from about 700 to 2000 psig.
  • a variety of catalysts may be utilized however, a preferred catalyst is di-tert.butyl peroxide which is added in benzene at the rate of about 0.5 to 2.0 lbs./1000 lbs. of polymer.
  • Residence time in the reactor is about 0.1 to about 1.0 hours or more. After the reaction mixture is removed from the reactor, the solvent and unreacted starting materials are stripped off yielding the terpolymer product.
  • propylene or butylene is grafted onto a backbone or basic chain which is a copolymer of ethylene and vinyl acetate.
  • the weight percent of propylene or butylene ranges from about 0.6 to about 5.0 and the weight percent of vinyl acetate is about 17 to about 40 with the balance being ethylene.
  • the number average molecular weights of these graft copolymers will range from about 4000 to about 80,000 or more.
  • the ethylene-vinyl acetate copolymers utilized in preparing the graft copolymers may be prepared by any convenient process, such as that of U.S. Pat. Nos. 3,048,479 and 3,215,678, by a free radical-initiated polymerization of ethylene and a vinyl acetate.
  • An especially useful group of ethylene-vinyl acetate copolymers are those manufactured by E. I. duPont de Nemours and sold under the tradename "Elvax". The characteristics of the various Elvax additives are given in Table I below:
  • the polymerization is conducted at temperatures of about 280° to about 340° F. and at pressures ranging from about 700 to about 2000 psig and, preferably, at about 750 to about 950 psig.
  • the autoclave employed containing the solvent such as benzene, toluene, etc. and the vinyl acetate is first purged about three times with nitrogen, twice with ethylene and then charged with sufficient ethylene to give the desired pressure when heated to the reaction temperature. Additional ethylene is added as the polymerization proceeds whenever it is needed.
  • the polymerization is considered to be complete when the pressure of the autoclave drops to less than about 60 psig.
  • the viscous copolymer is recovered by stripping off the solvent and any unreacted vinyl acetate which remains under vacuum.
  • Graft copolymers where the graft is propylene or butylene and the basic chain is a copolymer of ethylene and vinyl acetate can be made, for example, by redissolving an ethylene-vinyl acetate copolymer in benzene or other suitable hydrocarbon solvent, placing the copolymer solution in a stirred autoclave with the requisite amount of propylene or butylene together with a peroxide type catalyst and continuing the polymerization under the influence of heat and pressure. Temperatures of from about 250° to about 400° F. may be employed at autogenous pressure.
  • the amount of terpolymer or graft copolymer pour depressant incorporated into the residual fuel oil compositions of this invention may be varied over a wide range. Generally the amount of the terpolymer in the residual fuel oil composition will vary from about 0.01 to about 0.50 weight percent and preferably between about 0.02 to about 0.25 weight percent.
  • the required amount of vinyl acetate-ethylene-propylene or butylene terpolymer or the graft copolymer may be added with mixing directly to the residual fuel which is preferably heated.
  • the terpolymer or graft type copolymer is added to the residual fuel in solution form dissolved in a hydrocarbon such as toluene, kerosene, etc., at a temperature of about 30° to about 150° C. with mixing.
  • a terpolymer is prepared by introducing 10 parts of ethylene, 4.3 parts vinyl acetate, 0.1 part of propylene and 3 parts of benzene per hour into a stirred 2-liter autoclave maintained at a temperature of 140°-150° C. at 1450 psig.Di-tert. butyl peroxide is employed as the catalyst and is introduced in benzene into the reactor at the rate of 0.8 lbs./1000 lb. of polymer. The product is continuously removed from the reactor giving a residence time of 15 minutes. After the reaction mixture is removed from the reactor, it is stripped of solvent and unreacted materials yielding the terpolymer product.
  • the composition of the terpolymer is about 26 weight percent vinyl acetate, 0.6 weight percent of propylene with the balance being ethylene.
  • the number average molecular weight of the terpolymer as measured by vapor pressure osmometry is about 21,500.
  • a residual fuel oil composition is prepared by mixing at 185° F. for one hour 65 volume percent of F/18 residual fuel, about 35 volume percent of Louisiana No. 6 fuel oil and a sufficient amount of the above prepared terpolymer so that the concentration of the terpolymer is 0.15 weight percent.
  • the pour point of this composition is determined by the method of ASTM D-97 and found to be substantially below that of the same fuel oil mixture without terpolymer which exhibits a pour point of 80° F.
  • the pour point of the F/18 residual fuel alone is 95° F. while the pour point of the Louisiana No. 6 residual fuel is 30° F.
  • a graft polymer is made by dissolving one part of di-tert. butyl peroxide and ten parts of Elvax 410 in 90 parts of benzene in a stirred 2-liter autoclave.
  • the reactor is flushed three times with nitrogen and then twice with the olefin to be used as the grafting agent, i.e., propylene.
  • the reactor is heated to 300° F. for four hours during which time the grafting reaction occurs.
  • the product is removed from the reactor and stripped of solvent and unreacted materials.
  • the resulting polymer (Polymer I) about 2 parts of propylene is grafted onto 100 parts of Elvax 410.
  • a residual fuel oil composition is prepared by mixing at 200° F. for 1.5 hours 75 volume percent F/18 residual fuel and 25 volume percent of Louisiana No. 6 fuel oil and a sufficient amount of grafted Polymer I made above so that the concentration of the grafted polymer is 0.18 weight percent.
  • the pour point of this composition is determined by ASTM D-97 and found to be substantially below that of the same fuel oil mixture without the grafted copolymer which exhibits a pour point of 80° F. or with a similar concentration of Elvax 410 which exhibits a pour point slightly below 80° F.
  • this invention relates to an improved process for the transportation of the novel fuel oil compositions described in detail above.
  • the improved process of this invention for the pipeline transportation of the residual fuel oil composition described above comprises introducing into the said pipeline a residual fuel oil composition comprising a major amount of a high pour point, low sulfur waxy, residual fuel oil and a minor amount of a low wax, low pour residual fuel oil and an effective pour depressant amount of one of the useful terpolymers of this invention, such as the vinyl acetate-ethylene-propylene or butylene terpolymer or the graft copolymer previously described.
  • the amount of the terpolymer or graft copolymer will range from about 0.01 to about 0.50 weight percent.

Abstract

A low pour point residual fuel oil composition is prepared from a major amount of a high pour point, low sulfur, waxy, residual fuel and a minor amount of a low wax, low pour, residual fuel oil by adding thereto from 0.01 to 0.5% by weight of an oil soluble terpolymer such as vinyl acetate-ethylene-propylene or butylene or a graft copolymer in which propylene or butylene is grafted onto an ethylene-vinyl acetate copolymer backbone or basic chain, having preferably, a number average molecular weight of about 12,000 to about 60,000. In another aspect, this invention relates to a process for the pipeline transportation of the low pour residual fuel oil compositions previously described.

Description

BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention is concerned with means for providing a low sulfur, low pour fuel oil composition. More particularly, the invention is concerned with a fuel oil composition containing a major amount of a high pour, low sulfur, waxy residual fuel and a minor amount of a low wax, low pour, residual fuel oil, this blend having a reduced pour point relative to its components owing to the incorporation therein of a minor amount of an oil-soluble terpolymer or graft copolymer.
2. Description of the Prior Art
As is well known, residual fuel oils contain quantities of wax and asphaltic compounds which render them viscous and which sometimes interfere with practical use thereof. Particularly serious problems can be encountered in pumping residual fuel oils to a burner and in making them flow at low temperatures. Other factors to be reckoned with in regard to these oils are the facts that they behave as non-Newtonian liquids at low temperatures; exhibit variable solidifying temperatures and manifest peculiar hysteresis phenomena--all of which result in difficulties in equipment design.
One approach used in making these oils easier to handle has been to subject them to fairly lengthy and costly dewaxing procedures.
Another approach which has been suggested and tried in order to bring the viscosity of residual fuel oils to suitable levels has been to dilute or "cut" them with a major amount of lighter distillate oils. This procedure is expensive because of the considerably higher cost of the distillate oils relative to that of residual oils.
In recent years it has been recommended to incorporate additives in lubricating oils and in so-called middle distillates in order to tie in the wax present therein and to improve flow characteristics at reduced temperatures. The additives in question consist either of compounds formed by alkylating benzene or naphthalene derivatives; or, of copolymers of ethylene-vinyl fatty acid ester of a molecular weight up to 3,000 containing from 15 to 25 percent by weight of the vinyl fatty acid ester.
The main object of the present invention, accordingly, is to provide for critical blending of high pour waxy residual fuel oils with low waxy, low pour residual fuel oils to give large increases in pour reduction without employing elaborate dewaxing procedures.
An equally important object of the claimed invention is to provide a novel fuel oil blend characterized by a low sulfur content and a reduced pour point resulting from the incorporation therein of a small amount, for example, a terpolymer of vinyl acetate, ethylene and propylene or butylene.
A further object of the claimed invention is to provide a fuel oil blend which will be stable at different blend temperatures over prolonged storage times.
BRIEF DESCRIPTION OF THE INVENTION
In its broadest aspect this invention relates to fuel oil compositions having low pour points comprising a major amount of a high pour, low sulfur, waxy residual fuel, and a minor amount of a low wax, low pour residual fuel containing an effective pour depressant amount of an oil-soluble terpolymer or a graft copolymer. The terpolymer used in preparing the crude oil compositions of this invention is a vinyl acetate-ethylene, propylene or butylene terpolymer while the graft copolymer comprises an ethylene-vinyl acetate backbone or basic chain having grafted thereto propylene or butylene. In another aspect this invention relates to a process for the pipeline transportation of the above-described fuel oil compositions.
DETAILED DESCRIPTION OF THE INVENTION
The residual fuel oil composition of this invention comprises a major amount (i.e., over 50 percent by volume) of a high pour, low sulfur waxy, residual fuel oil having an API gravity of about 20.0 to about 25.0; a sulfur content of between about 0.40 wt. % and about 0.96 wt. %; a Furol viscosity at 122° F. of about 60 to about 230; a flash point of between about 300° and 450° F., with a wax content of between about 10 and 20 percent; and a minor amount (i.e. less than 50 percent by volume) of a low waxy, low pour residual fuel oil having an API gravity of about 10.0 to about 15.0; a Furol viscosity at 122° F. of about 150 to about 250; a flash point of about 220° to about 350° F.; a pour point of between about 25° F. and about 45° F., a wax content of between about 2 and 5 weight percent with a sulfur content of between about 0.50 and about 0.90 weight percent. A waxy, low pour residual fuel oil which has given particularly good results as the minor constituent of the claimed blend is that known as No. 6 Fuel Oil (Is this Louisiana No. 6?) which has an API gravity of about 12.3, a Furol viscosity of 207.0 at 122° F., a pour point of about 40° F. and a wax content of about 3 percent.
Preferably, the residual fuel oil compositions of this invention will contain about 55 to about 85 volume percent of the high pour, low sulfur, waxy residual fuel; about 45 to 15 volume percent of the low wax, low pour residual fuel and about 0.01 to about 0.5 weight percent of the oil soluble terpolymer or graft type copolymer.
One type of oil-soluble terpolymers useful in preparing the crude oil compositions of this invention comprises recurring units of vinyl acetate, ethylene and propylene or butylene.
The number average molecular weight of the vinyl acetate-ethylene-propylene or butylene terpolymer utilized in this invention as previously described will range from about 5000 to about 80,000 or more and preferably will be from about 12,000 to about 60,000 as determined by vapor pressure osmometry.
In the vinyl acetate-ethylene-propylene or butylene terpolymer the weight percent of the vinyl acetate units is about 10 to about 45; the weight percent propylene or butylene units is about 0.01 to about 5.0 with the ethylene units being the balance.
Preparation of the vinyl acetate-ethylene-propylene or butylene terpolymer is conducted using processes well known in the art. For example, ethylene, vinyl acetate, and propylene in benzene are reacted in a stirred autoclave at a temperature of about 130° to about 150° C. and under pressures ranging from about 700 to 2000 psig. A variety of catalysts may be utilized however, a preferred catalyst is di-tert.butyl peroxide which is added in benzene at the rate of about 0.5 to 2.0 lbs./1000 lbs. of polymer. Residence time in the reactor is about 0.1 to about 1.0 hours or more. After the reaction mixture is removed from the reactor, the solvent and unreacted starting materials are stripped off yielding the terpolymer product.
In the graft copolymers utilized in this invention, propylene or butylene is grafted onto a backbone or basic chain which is a copolymer of ethylene and vinyl acetate. The weight percent of propylene or butylene ranges from about 0.6 to about 5.0 and the weight percent of vinyl acetate is about 17 to about 40 with the balance being ethylene. The number average molecular weights of these graft copolymers will range from about 4000 to about 80,000 or more.
The ethylene-vinyl acetate copolymers utilized in preparing the graft copolymers may be prepared by any convenient process, such as that of U.S. Pat. Nos. 3,048,479 and 3,215,678, by a free radical-initiated polymerization of ethylene and a vinyl acetate. An especially useful group of ethylene-vinyl acetate copolymers are those manufactured by E. I. duPont de Nemours and sold under the tradename "Elvax". The characteristics of the various Elvax additives are given in Table I below:
              TABLE I                                                     
______________________________________                                    
            % Vinyl Acetate                                               
"Elvax"     in Copolymer    Melt Index*                                   
______________________________________                                    
 40         39-42           45-70                                         
150         32-34           22-28                                         
210         27-29           335-465                                       
220         27-29           125-175                                       
240         27-29           22-28                                         
250         27-29           12-18                                         
260         27-29           5-7                                           
310         24-26           335-465                                       
350         24-26           16-22                                         
360         24-26           1.6-2.4                                       
410         17-19           430-580                                       
460         17-19           2.1-2.9                                       
______________________________________                                    
 *in g/10 min. as determined by ASTM 1328 modified.
In preparing the ethylene-vinyl acetate copolymers generally the polymerization is conducted at temperatures of about 280° to about 340° F. and at pressures ranging from about 700 to about 2000 psig and, preferably, at about 750 to about 950 psig. The autoclave employed containing the solvent such as benzene, toluene, etc. and the vinyl acetate is first purged about three times with nitrogen, twice with ethylene and then charged with sufficient ethylene to give the desired pressure when heated to the reaction temperature. Additional ethylene is added as the polymerization proceeds whenever it is needed. Generally the polymerization is considered to be complete when the pressure of the autoclave drops to less than about 60 psig. The viscous copolymer is recovered by stripping off the solvent and any unreacted vinyl acetate which remains under vacuum.
Graft copolymers where the graft is propylene or butylene and the basic chain is a copolymer of ethylene and vinyl acetate, can be made, for example, by redissolving an ethylene-vinyl acetate copolymer in benzene or other suitable hydrocarbon solvent, placing the copolymer solution in a stirred autoclave with the requisite amount of propylene or butylene together with a peroxide type catalyst and continuing the polymerization under the influence of heat and pressure. Temperatures of from about 250° to about 400° F. may be employed at autogenous pressure.
The amount of terpolymer or graft copolymer pour depressant incorporated into the residual fuel oil compositions of this invention may be varied over a wide range. Generally the amount of the terpolymer in the residual fuel oil composition will vary from about 0.01 to about 0.50 weight percent and preferably between about 0.02 to about 0.25 weight percent.
The required amount of vinyl acetate-ethylene-propylene or butylene terpolymer or the graft copolymer may be added with mixing directly to the residual fuel which is preferably heated. Preferably, the terpolymer or graft type copolymer is added to the residual fuel in solution form dissolved in a hydrocarbon such as toluene, kerosene, etc., at a temperature of about 30° to about 150° C. with mixing.
The following examples which illustrate this invention are to be considered not limitative.
EXAMPLE I
A terpolymer is prepared by introducing 10 parts of ethylene, 4.3 parts vinyl acetate, 0.1 part of propylene and 3 parts of benzene per hour into a stirred 2-liter autoclave maintained at a temperature of 140°-150° C. at 1450 psig.Di-tert. butyl peroxide is employed as the catalyst and is introduced in benzene into the reactor at the rate of 0.8 lbs./1000 lb. of polymer. The product is continuously removed from the reactor giving a residence time of 15 minutes. After the reaction mixture is removed from the reactor, it is stripped of solvent and unreacted materials yielding the terpolymer product. The composition of the terpolymer is about 26 weight percent vinyl acetate, 0.6 weight percent of propylene with the balance being ethylene. The number average molecular weight of the terpolymer as measured by vapor pressure osmometry is about 21,500.
A residual fuel oil composition is prepared by mixing at 185° F. for one hour 65 volume percent of F/18 residual fuel, about 35 volume percent of Louisiana No. 6 fuel oil and a sufficient amount of the above prepared terpolymer so that the concentration of the terpolymer is 0.15 weight percent. The pour point of this composition is determined by the method of ASTM D-97 and found to be substantially below that of the same fuel oil mixture without terpolymer which exhibits a pour point of 80° F. The pour point of the F/18 residual fuel alone is 95° F. while the pour point of the Louisiana No. 6 residual fuel is 30° F.
EXAMPLE II
A graft polymer is made by dissolving one part of di-tert. butyl peroxide and ten parts of Elvax 410 in 90 parts of benzene in a stirred 2-liter autoclave. The reactor is flushed three times with nitrogen and then twice with the olefin to be used as the grafting agent, i.e., propylene. The reactor is heated to 300° F. for four hours during which time the grafting reaction occurs. The product is removed from the reactor and stripped of solvent and unreacted materials. In the resulting polymer (Polymer I) about 2 parts of propylene is grafted onto 100 parts of Elvax 410.
A residual fuel oil composition is prepared by mixing at 200° F. for 1.5 hours 75 volume percent F/18 residual fuel and 25 volume percent of Louisiana No. 6 fuel oil and a sufficient amount of grafted Polymer I made above so that the concentration of the grafted polymer is 0.18 weight percent. The pour point of this composition is determined by ASTM D-97 and found to be substantially below that of the same fuel oil mixture without the grafted copolymer which exhibits a pour point of 80° F. or with a similar concentration of Elvax 410 which exhibits a pour point slightly below 80° F.
In another aspect, this invention relates to an improved process for the transportation of the novel fuel oil compositions described in detail above.
The improved process of this invention for the pipeline transportation of the residual fuel oil composition described above comprises introducing into the said pipeline a residual fuel oil composition comprising a major amount of a high pour point, low sulfur waxy, residual fuel oil and a minor amount of a low wax, low pour residual fuel oil and an effective pour depressant amount of one of the useful terpolymers of this invention, such as the vinyl acetate-ethylene-propylene or butylene terpolymer or the graft copolymer previously described. Generally, the amount of the terpolymer or graft copolymer will range from about 0.01 to about 0.50 weight percent.

Claims (9)

What is claimed is:
1. A low pour residual fuel oil composition comprising a major amount of a high pour point, low sulfur, waxy, residual fuel and a minor amount of a low wax, low pour residual fuel oil and an effective pour depressant amount of an oil-soluble polymer selected from the group consisting of a terpolymer comprising recurring units of vinyl acetate, ethylene and an olefin selected from the group consisting of propylene and butylene and a graft copolymer comprising an ethylene-vinyl acetate copolymer backbone having grafted thereto an olefin selected from the group consisting of propylene and butylene.
2. The composition of claim 1 wherein the said oil-soluble polymer is a graft copolymer wherein the number average molecular weight of the said copolymer is from about 4000 to about 60,000; wherein the weight percent of vinyl acetate in the said graft copolymer is about 17 to about 40, and the weight percent of propylene or butylene is about 0.6 to about 5.0 with the balance being ethylene.
3. The composition of claim 1 wherein the said oil-soluble polymer is a terpolymer which comprises about 15 to about 28 weight percent vinyl acetate, from about 0.1 to about 5.0 weight percent propylene or butylene with the balance being ethylene.
4. The composition of claim 1 wherein the said oil-soluble polymer is a terpolymer which comprises about 26 percent by weight of propylene with the balance being ethylene.
5. The composition of claim 3 wherein the number average molecular weight of the said terpolymer will range from about 5000 to about 80,000.
6. The composition of claim 3 wherein the number average molecular weight of the said terpolymer will range from about 12,000 to about 60,000.
7. In the transportation of residual fuel oils, the improvement which comprises introducing into a pipeline a low pour residual fuel composition comprising a major amount of a high pour point, low sulfur waxy residual fuel and a minor amount of a low wax, low pour residual fuel and an effective pour depressant amount of an oil-soluble polymer selected from the group consisting of a terpolymer comprising recurring units of vinyl acetate, ethylene and an olefin selected from the group consisting of propylene and butylene and a graft copolymer comprising an ethylene-vinyl acetate copolymer backbone having grafted thereto an olefin selected from the group consisting of propylene and butylene.
8. The process of claim 7 wherein the said oil-soluble polymer is a terpolymer which comprises about 15 to about 28 weight percent vinyl acetate, from about 0.1 to about 5.0 weight percent propylene or butylene with the balance being ethylene.
9. The process of claim 7 wherein the said oil-soluble polymer is a terpolymer which comprises about 26 percent by weight vinyl acetate, about 0.6 percent by weight of propylene with the balance being ethylene.
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Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4564460A (en) 1982-08-09 1986-01-14 The Lubrizol Corporation Hydrocarbyl-substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4575526A (en) 1982-08-09 1986-03-11 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylaging agent derivative containing combinations, and fuels containing same
EP0184083A2 (en) * 1984-11-29 1986-06-11 Hoechst Aktiengesellschaft Terpolymers of ethylene, process for their manufacture and their use
US4613342A (en) 1982-08-09 1986-09-23 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
EP0196217A2 (en) * 1985-03-25 1986-10-01 Amoco Corporation Ethylene-unsaturated, ester-substituted olefin terpolymer flow improvers
US4623684A (en) 1982-08-09 1986-11-18 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4769043A (en) * 1984-08-20 1988-09-06 Texaco Inc. Oil containing dispersant VII olefin copolymer
US4862908A (en) * 1986-07-17 1989-09-05 Ruhrchemie Aktiengesellschaft Mineral oils and mineral oil distillates having improved flowability and method for producing same
US4932980A (en) * 1987-07-29 1990-06-12 Rohm Gmbh Polymeric fluidizer for middle distillates
US5256166A (en) * 1984-12-06 1993-10-26 National Distillers And Chemical Corporation Terpolymer of ethylene, vinyl acetate and isobutylene useful as pour point depressants in distillate oils
US5681359A (en) * 1996-10-22 1997-10-28 Quantum Chemical Corporation Ethylene vinyl acetate and isobutylene terpolymer as a cold flow improver for distillate fuel compositions
WO2000069998A1 (en) * 1999-05-13 2000-11-23 Equistar Chemicals, L.P. Cold flow improvers for distillate fuel compositions
US6206939B1 (en) 1999-05-13 2001-03-27 Equistar Chemicals, Lp Wax anti-settling agents for distillate fuels
US6342081B1 (en) 1999-07-13 2002-01-29 Equistar Chemicals, Lp Cloud point depressants for middle distillate fuels
US6673131B2 (en) 2002-01-17 2004-01-06 Equistar Chemicals, Lp Fuel additive compositions and distillate fuels containing same
US20080016753A1 (en) * 2006-07-18 2008-01-24 Clariant International Ltd. Additives for improving the cold properties of fuel oils
US20080016754A1 (en) * 2006-07-18 2008-01-24 Clariant International Ltd. Additives for improving the cold properties of fuel oils
US20080016755A1 (en) * 2006-07-18 2008-01-24 Clariant International Ltd. Additives for improving the cold properties of fuel oils
CN105199030A (en) * 2015-11-03 2015-12-30 西安长庆化工集团有限公司 Drag reducer with pour-point depression function and preparation method of drag reducer
CN105953075A (en) * 2016-05-11 2016-09-21 中化工储运有限公司 Long-distance conveying method for heavy fuel oil

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Cited By (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4623684A (en) 1982-08-09 1986-11-18 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4575526A (en) 1982-08-09 1986-03-11 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylaging agent derivative containing combinations, and fuels containing same
US4564460A (en) 1982-08-09 1986-01-14 The Lubrizol Corporation Hydrocarbyl-substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4613342A (en) 1982-08-09 1986-09-23 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4769043A (en) * 1984-08-20 1988-09-06 Texaco Inc. Oil containing dispersant VII olefin copolymer
EP0184083A3 (en) * 1984-11-29 1987-02-04 Ruhrchemie Aktiengesellschaft Terpolymers of ethylene, process for their manufacture and their use
EP0184083A2 (en) * 1984-11-29 1986-06-11 Hoechst Aktiengesellschaft Terpolymers of ethylene, process for their manufacture and their use
US5256166A (en) * 1984-12-06 1993-10-26 National Distillers And Chemical Corporation Terpolymer of ethylene, vinyl acetate and isobutylene useful as pour point depressants in distillate oils
EP0196217A2 (en) * 1985-03-25 1986-10-01 Amoco Corporation Ethylene-unsaturated, ester-substituted olefin terpolymer flow improvers
EP0196217A3 (en) * 1985-03-25 1986-11-26 Amoco Corporation Ethylene-unsaturated, ester-substituted olefin terpolymer flow improvers
US4746327A (en) * 1985-03-25 1988-05-24 Standard Oil Company (Indiana) Ethylene-unsaturated, ester-substituted olefin terpolymer flow improvers
US4862908A (en) * 1986-07-17 1989-09-05 Ruhrchemie Aktiengesellschaft Mineral oils and mineral oil distillates having improved flowability and method for producing same
US4932980A (en) * 1987-07-29 1990-06-12 Rohm Gmbh Polymeric fluidizer for middle distillates
US5681359A (en) * 1996-10-22 1997-10-28 Quantum Chemical Corporation Ethylene vinyl acetate and isobutylene terpolymer as a cold flow improver for distillate fuel compositions
WO2000069998A1 (en) * 1999-05-13 2000-11-23 Equistar Chemicals, L.P. Cold flow improvers for distillate fuel compositions
US6203583B1 (en) * 1999-05-13 2001-03-20 Equistar Chemicals, Lp Cold flow improvers for distillate fuel compositions
US6206939B1 (en) 1999-05-13 2001-03-27 Equistar Chemicals, Lp Wax anti-settling agents for distillate fuels
US6342081B1 (en) 1999-07-13 2002-01-29 Equistar Chemicals, Lp Cloud point depressants for middle distillate fuels
US6673131B2 (en) 2002-01-17 2004-01-06 Equistar Chemicals, Lp Fuel additive compositions and distillate fuels containing same
US20080016755A1 (en) * 2006-07-18 2008-01-24 Clariant International Ltd. Additives for improving the cold properties of fuel oils
US20080016754A1 (en) * 2006-07-18 2008-01-24 Clariant International Ltd. Additives for improving the cold properties of fuel oils
US20080016753A1 (en) * 2006-07-18 2008-01-24 Clariant International Ltd. Additives for improving the cold properties of fuel oils
DE102006033150B4 (en) * 2006-07-18 2008-10-16 Clariant International Limited Additives for improving the cold properties of fuel oils
US8961622B2 (en) 2006-07-18 2015-02-24 Clariant Finance (Bvi) Limited Additives for improving the cold properties of fuel oils
US8968428B2 (en) 2006-07-18 2015-03-03 Clariant Produkte (Deutschland) Gmbh Additives for improving the cold properties of fuel oils
US8979951B2 (en) 2006-07-18 2015-03-17 Clariant Finance (Bvi) Limited Additives for improving the cold properties of fuel oils
CN105199030A (en) * 2015-11-03 2015-12-30 西安长庆化工集团有限公司 Drag reducer with pour-point depression function and preparation method of drag reducer
CN105199030B (en) * 2015-11-03 2017-08-25 西安长庆化工集团有限公司 A kind of pour point depressing and drag reducing agent and preparation method thereof
CN105953075A (en) * 2016-05-11 2016-09-21 中化工储运有限公司 Long-distance conveying method for heavy fuel oil

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